Classifications

• • C—CHEMISTRY; METALLURGY
  • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
  • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
  • C02F3/00—Biological treatment of water, waste water, or sewage
  • C02F3/02—Aerobic processes
  • C02F3/12—Activated sludge processes
  • C02F3/1205—Particular type of activated sludge processes
  • C02F3/121—Multistep treatment
• • C—CHEMISTRY; METALLURGY
  • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
  • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
  • C02F3/00—Biological treatment of water, waste water, or sewage
  • C02F3/02—Aerobic processes
  • C02F3/12—Activated sludge processes
  • C02F3/1205—Particular type of activated sludge processes
  • C02F3/1221—Particular type of activated sludge processes comprising treatment of the recirculated sludge
• • C—CHEMISTRY; METALLURGY
  • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
  • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
  • C02F3/00—Biological treatment of water, waste water, or sewage
  • C02F3/02—Aerobic processes
  • C02F3/12—Activated sludge processes
  • C02F3/1236—Particular type of activated sludge installations
  • C02F3/1263—Sequencing batch reactors [SBR]
• • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
  • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
  • Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
  • Y02W10/00—Technologies for wastewater treatment
  • Y02W10/10—Biological treatment of water, waste water, or sewage

Definitions

• the present invention relates to a process for the disinfection and aerobic stabilization of concentrated sewage sludge in several steps, employing one or more heat-insulated containers, preferably with stirring, with the addition of oxygen-containing gas.
• the quality of the issuing sludge liquor is often unsatisfactory; this sludge liquor, in general is recycled into the biological waste water purification.
• the sewage sludge, aerobically stabilized and disinfected in accordance with the known process has been used in the past as a fertilizer. However, this use has been restricted by recent laws and regulations so that in the future the sewage sludge obtained will often have to be disposed of or combusted. Thus, it is of particular importance that the treated sewage sludge can be readily thickened and dehydrated and that a sludge liquor water is obtained which has a low residual contamination.
• the object of the invention to develop a process for the disinfection and aerobic stabilization of concentrated sewage sludge in several steps, using one or more heat-insulated containers, preferably with stirring, with the addition of oxygen-containing gas.
• the process works safely and reliably, disinfects and stabilizes perfectly, even under conditions of varying crude sewage sludge input, varying temperatures of the crude sewage sludge, and/or the environment.
• the process avoids unacceptable odor problems, is comparable to current processes in cost aspects and provides a well-settling sludge with a water effluent of low contamination.
• the sludge is disinfected by further aerobic degradation without supplying external heat at about 50° C. to 55° C. for at least 20 hours or at >55° C. for at least 10 hours, and
• the sludge is stabilized at mesophilic temperature by active cooling to from 25° C. to 45° C. and further aerobic degradation within from 2 to 8 days, and preferably within from 3 to 5 days.
• the steps (a), (b) and (c) are carried out in the same container.
• That container is furnished with a heat exchanger, for example one using pipe coils or flushable plate-coolers, in order to optionally pre-heat the concentrated crude sludge, but mostly to carry away the heat at the end of step (b) and during the step (c) and thereby to effect the active cooling.
• a heat exchanger for example one using pipe coils or flushable plate-coolers
• That one container-process in order to effectively utilize the heat to be removed at the end of step (b) and, in addition, to increase the flexibility of the process, may be extended in that two or more batches are run in two or more containers at different times so that the amount of heat recovered at the beginning of step (c) of a preceding batch is employed for pre-heating the concentrated crude sludge of step (a) of a subsequent batch.
• three or more containers can be provided and another embodiment of the process can be used, which is particularly simple and economical, in which embodiment the steps (a), (b) and (c) are allowed to take place in three separate stages A, B and C connected in series, wherein the containers of the stages B and C have capacities several times the capacity of the container of stage A.
• the heating of the crude sludge in stage A is generally effected by way of heat exchange with the sludge in stage C. However, it is also possible to effect the heating of the crude sludge in stage A by way of a heat exchange with the sludge of stage B. If desired, heat may be extracted also from the effluent from stage C.
• stage C it has been found that in the regular operation of stage C, more heat is released and has to be removed than is required for warming the concentrated crude sludge in stage A. Thus, amounts of heat from stage C exceeding the amount of heat needed in stage A are removed by heat exchange and can be utilized otherwise, if desired.
• stage A it is of course possible to satisfy the heat requirements of stage A also in part by means of a heat exchange with the sludge in stage B.
• heat may be transferred to stage A from stage B in order to further increase the temperature in the former stage.
• the temperature in stage A must be at least 25° C. prior to transferring a batch to stage B. Temperatures in excess of 45° C. occur rarely in stage A, because even with stronger aeration in stage A, the temperature rise due to aerobic degradation is not so fast that the maximum temperatures of stage C will be essentially exceeded.
• the supply to stage A may be batch or continuous. Stage A is preferably agitated and aerated, but this is not absolutely required.
• the aerobic degradation in stage B is so vigorous that temperatures in excess of 50° C. will be generated. At temperatures between 50° C. and 70° C., with appropriate residence times, the disinfection is safely assured.
• the time between two feeding cycles can be made to depend on the temperature in stage B. At 50° C., a time between two feeding cycles of one day will be sufficient. With temperatures in excess of 65° C., even a time between two feeding cycles of three hours will be sufficient to obtain a perfect disinfection. However, as a safety measure, disinfection should be carried out for at least ten hours.
• the temperature in stage B can be controlled by the amount of the oxygen supply. In addition, it may also be made to depend on the time available between two feeding cycles.
• the variation in the amounts of concentrated crude sludge to be processed can be compensated by an appropriate adaption of the filling height in the containers and, if necessary, by turning on or off additional containers connected in parallel or in series and operating for the respective stage.
• stage C the temperature is reduced to from 25° C. to 45° C., and preferably to about 35° C. At these temperatures there is formed a sludge which has an especially good settling behavior and an effluent with low contamination.
• the average residence times in general are:
• a concentrated sewage sludge as that from mechanical and/or biological purification of sewage or industrial waste waters, wherein a solids content of from 2 to 8% has been attained by static and/or machine concentration.
• Such concentrated sewage sludges in general, have a sufficient content of degradable matter required for the exothermal aerobic degradation in stage B, while, on the other hand, they still have rheological properties so that they are easy to handle.
• the supply of the oxygen-containing gas is generally effected by aeration. In special cases, more or less pure oxygen may be added as well. Oxygen-containing gases having an oxygen-content of less than 15% are only used as an exception, because then the oxygen supply becomes increasingly uneconomical. Furthermore, with such low-oxygen gases care is needed to ensure that anaerobic degradation is avoided, since this results in an odor problem.
• the oxygen supply may be controlled by the intensity of aeration and/or the oxygen content of the gas supplied.
• Agitation and aeration in the stages B and C and, optionally, in stage A can be effected by any means known in waste water technology and process technology.
• Aerating stirrers such as those manufactured, for example, by the company Fuchs Gas- und Wasser-technik, Mayen, have proven to be particularly useful in the process of the invention.
• the containers may be any of the reactors equipped with a stirrer and gas-introducing means as conventionally used in waste water technology, which reactors preferably may also be provided with additional foam cutters and foam controllers. Heat supply and removal is effected by means of conventional heat exchangers. Undesirable heat losses are eliminated by providing the containers with a sufficient heat insulation.
• the process of the invention can be employed not only for the disinfection and aerobic stabilization of sewage sludge, but also for the treatment of liquid manure and other organic concentrates such as yeast wastes, etc.. It has been shown that the process of the invention reliably and flexibly results in disinfection and good stabilization, whereby a well-settling sewage sludge and a sludge liquor of good quality and low residual contamination are formed. In contrast to only thermophilic or anaerobic degradation processes, no odor nuisance is produced. Due to the mesophilic residue stabilization, ammonium is also largely subjected to nitrification, whereby the pH value decreases from a value in excess of 8 to the neutral range or somewhat lower.

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• Life Sciences & Earth Sciences (AREA)
• Biodiversity & Conservation Biology (AREA)
• Microbiology (AREA)
• Hydrology & Water Resources (AREA)
• Engineering & Computer Science (AREA)
• Environmental & Geological Engineering (AREA)
• Water Supply & Treatment (AREA)
• Chemical & Material Sciences (AREA)
• Organic Chemistry (AREA)
• Treatment Of Sludge (AREA)
• Immobilizing And Processing Of Enzymes And Microorganisms (AREA)
• Aeration Devices For Treatment Of Activated Polluted Sludge (AREA)
• Physical Water Treatments (AREA)
• Measuring Volume Flow (AREA)
• Apparatus For Radiation Diagnosis (AREA)
• External Artificial Organs (AREA)
• Investigating Or Analysing Materials By Optical Means (AREA)
• Activated Sludge Processes (AREA)

Applications Claiming Priority (4)

Publications (1)

Family

ID=25878010

Family Applications (1)

Country Status (8)

Cited By (15)

Families Citing this family (4)

Citations (8)

• 1990
  • 1990-01-28 DE DE9090101672T patent/DE59001181D1/de not_active Expired - Fee Related
  • 1990-01-28 ES ES90101672T patent/ES2039968T3/es not_active Expired - Lifetime
  • 1990-01-28 AT AT90101672T patent/ATE88166T1/de not_active IP Right Cessation
  • 1990-01-28 DK DK90101672T patent/DK0384162T3/da active
  • 1990-01-28 EP EP19900101672 patent/EP0384162B1/de not_active Expired - Lifetime
  • 1990-02-15 CA CA 2010156 patent/CA2010156C/en not_active Expired - Fee Related
  • 1990-02-21 TR TR19890A patent/TR26660A/xx unknown
  • 1990-02-21 US US07/483,045 patent/US4983298A/en not_active Expired - Lifetime

Patent Citations (8)

Non-Patent Citations (2)

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